WO2009010164A1

WO2009010164A1 - Device and method for processing cleaning fluids

Info

Publication number: WO2009010164A1
Application number: PCT/EP2008/005156
Authority: WO
Inventors: Martin Nissen; Klaus Wasmuht; Kurt Stippler; Cornelia Stumpe; Jan Momsen; Timm Kirchhoff
Original assignee: Krones Ag
Priority date: 2007-07-16
Filing date: 2008-06-25
Publication date: 2009-01-22
Also published as: CN101772375B; ES2387470T3; US20100224575A1; BRPI0812648A2; CA2693474A1; CN101772375A; PL2167222T3; RU2440180C2; MX2010000609A; EP2016992B1; EP2167222A1; EP2016992A1; CA2693474C; EP2167222B1; ES2393289T3; PL2016992T3; RU2010101629A

Abstract

The invention relates to an improved device and a method for processing cleaning fluids, the device comprising: at least one flushable coarse filter for coarsely filtering the cleaning fluid, a cross-flow filter for finely filtering the coarse filtrate from the at least one coarse filter, a return line through which the coarse filtrate is fed through the cross-flow filter in a circuit, a flushing device for flushing the coarse filter, a drain branching off from the circuit and connected to the flushing device for flushing the coarse filter with the coarse filtrate fed through the cross-flow filter in the circuit.

Description

DEVICE AND METHOD FOR PREPARING CLEANING LIQUID

Keiten

The invention relates to a method and an apparatus for processing of, in particular in the bottle cleaning or in CIP systems, z. B. in the brewhouse cleaning in breweries resulting cleaning fluids.

However, the method according to the invention and the device according to the invention are also particularly suitable for cleaning liquids which are obtained in food-processing enterprises, pharmaceutical operations or plastics recycling operations.

In breweries, the brewing vessel cleaning, as well as the bottle cleaning, with the help of cleaning lye. Bottles are cleaned, for example, with a bottle cleaning system, as shown roughly schematically in FIG. Such bottle washing systems 10 include, as will be described in detail later, for example, a pre-wash bath 32, a main wash bath 28, and a after-bath 37 as a first rinse zone. In the bottle cleaning, however, the condition of the cleaning liquor deteriorates despite the increase because more and more sludge settles and soluble, insoluble or colloidally dissolved components are contained in the liquor. These include u. a. Paper fibers from shredded labels, color pigments, binders from labels, wet strength agents, sizing agents, precipitated sludge from limescale components, adhering dirt from bottles, etc. When cleaning brewhouse containers, u. a. larger amounts of spent grains and trub residues as well as deposits from the cooking vessels for mash and wort boiling.

As a cleaning liquid, however, not only cleaning liquors are used. In particular, in CIP systems are used as cleaning fluids and acids and disinfectants that need to be cleaned, above all, the sludge that settles to the bottom of the CIP container before each cleaning step must be drained into the channel.

The preparation of the corresponding cleaning fluids is nowadays increasingly by filtration. The cleaning systems used in the prior art, however, the problem arises that the filter surfaces, in particular by the large men- to impurities, such as paper fibers from label residues, spent grains and Trubresten after a short time enforce. Such cleaning systems are therefore very maintenance-intensive and can not be operated continuously. In particular, in the cross-flow filtration of cleaning fluid to prevent the concentration of pollution in the cross-flow filter circuit, large-volume feedback containers are used. This has the disadvantage that at the end of the week, the large tank volume must be discarded. The large volumes in the filtration unit lead to increased heat radiation and reduced availability, since it is necessary to refill the tubs of the bottle washing machine when the filtration system is put into operation, which means considerable bottling downtimes.

Proceeding from this, the object of the present invention is to provide an apparatus and a method for treating cleaning liquids in order to clean the heavily soiled cleaning liquids in a simple, environmentally friendly and continuous manner.

According to the invention, this object is solved by the features of claims 1 and 10.

By a combination of coarse and fine filter or microfilter there is the advantage that the filter assembly, in particular the cross-flow filter (fine filter) is not added so quickly. It cleverly uses a cross-flow filter. The term cross-flow filter is a term that refers to filters in which the unfiltered material flows in parallel along a filter membrane. Part of the unfiltrate penetrates the membrane transversely to the flow direction of the filtrate and can be discharged as filtrate. In the process, solids of the unfiltered material are deposited on the membrane of the filter. With the parallel influx of the membrane, the depositing solids are continuously entrained by the liquid flow, so that a balance between re-allocation and cleaning of the membrane is achieved on the membrane.

According to the invention, a return line is provided, which leads the roughly filtered cleaning liquid, ie the coarse filtrate of the coarse filter in a circle through the cross-flow filter. Thus, sufficient flow and filter efficiency can be ensured. In order now to skilfully prevent the concentration of impurities in the circulating coarse filtrate, a derivative is provided which branches off from the circuit, in particular from the return line and with a backwashing connected is. Thus, the cleaning liquid concentrated with impurities can be skilfully used for backwashing the coarse filter. This means that, on the one hand, by diverting the coarse filtrate, a concentration of contamination can be prevented, on the other hand, this derived coarse filtrate is used in an efficient way for backwashing and must not be discarded. The present invention allows no additional tank to buffer the concentrate build up. This has the further advantage that at the end of the week no large tank volume must be discarded. Because the system does not have a large tank volume, the entire system may be under pressure resulting in minimized pumping power. In addition, small filling volumes offer the advantage that the availability, for example of a bottle cleaning machine, increases since it is not necessary to refill the bottle cleaning machine when starting up the filtration system. Furthermore, it is advantageous that, for example, both for the preparation of lye and for the treatment of the main liquor of a bottle washer the same flow scheme is applicable. This allows a simplified production in which, depending on the application, only the cross-flow filter, ie the pore size of the corresponding membrane, must be adjusted. Cleaning liquids are to be understood as meaning both cleaning liquor and cleaning acid or disinfectant.

Advantageously, the device has at least two coarse filters which are arranged in parallel and can be backwashed in alternation. Thus, a continuous process can be ensured because even if one of the coarse filters is being backwashed and cleaned, the second coarse filter is in use. Since the circulated coarse filtrate is used for backwashing, a backwashing can thus often be carried out, which improves the filter efficiency. The process does not have to be interrupted.

Advantageously, the coarse filter filters out particles of a size> 50 μm. Depending on the application, the cross-flow filter has a pore size in a range of <= 2 μm, preferably <= 0.4 μm. According to a preferred embodiment, a disc filter can be used as a coarse filter. Such a disc filter is easily backwashed.

According to a preferred embodiment, the apparatus prepares, as a cleaning liquor, main liquor from a main wash bath of a bottle cleaning machine and comprises a fine filtrate conduit, which again renders the fine filtrate from the cross-flow filter to the main body. tepid. The device according to the invention is at the same time also suitable for the treatment of afterglow from a Nachlaugebad a bottle washing machine and then includes a fine filtrate, which feeds the fine filtrate from the cross-flow filter again the Nachlaugebad.

When treating main liquor, the circuit may include another branch conduit for discarding a portion of the recycled coarse filtrate. Thus, if the concentration of impurities in the cross-flow filter circuit becomes too large, in addition, a part of the circulated coarse filtrate can be branched off and discarded, so that the concentration of the impurity decreases. Thus, excessive gel layer formation on the membrane surface of the cross-flow filter and premature clogging can be prevented.

In the purification of lye, the circuit may also comprise a further branch line for feeding a part of the circulated coarse filtrate to a pre-leaching bath. Thus, the concentration of impurities in the membrane filtration circuit can be prevented in an advantageous manner, wherein the coarse filtrate can still be used for the Vorlaugebad at the same time, since the cleaning liquor does not need to be filtered so much in Vorlaugebad.

According to the present invention, cleaning solution or acid or disinfecting liquid can also be prepared as a cleaning liquid from a CIP system, the fine filtrate then being supplied to a corresponding alkali or acid or disinfecting liquid tank.

In the method according to the invention, a certain part of the circulated coarse filtrate can be continuously removed. The discharged part of the coarse filtrate can also be removed in cycles at intervals during the filtration process.

The present invention will be explained in more detail below with reference to the following figures.

Figure 1 shows schematically the flow diagram of a device according to the present invention. Figure 2a shows schematically a section through a disc filter used in the device according to the invention.

FIG. 2b schematically shows a plan view of a pane of the pane filter shown in FIG. 2a.

Figure 3 shows schematically the different stages of a bottle cleaning system.

FIG. 4 shows, roughly schematically, a section through a cross-flow filter.

FIG. 5 shows a section along the line I-I in FIG. 4.

FIG. 6 shows a perspective view of a multi-tubular membrane filter cartridge which is used, for example, in the filter shown in FIG.

Figure 7 shows schematically the basic scheme of a CIP system.

According to the present invention, a backwashable coarse filter, for example a disc filter 2, in combination with a cross-flow filter 3 is used to treat the contaminated cleaning liquids obtained in breweries.

A disc filter is shown for example in FIGS. 2a and 2b. The disc filter has a filter housing 20, as well as a Unfiltratzulauf 21 and a coarse filtrate outlet 22. Via the inlet 21, the cleaning liquid is supplied to the disc filter 2 according to the present invention. The disk filter 2 has a plurality of filter disks 17 arranged one above the other. As is apparent from Figure 2b, the filter discs 17 are constructed as filter rings. The discs 17 are compressed by the spring force of the spring 19. The discs have a corrugation 18 on at least one side. Advantageously, the grooves or elevations 18 extend substantially radially outwardly. The corrugation of the superposed discs 17 thus give the filter pores through which the unfiltered material passes through the filter. Plastic discs are preferably used here. The non-filtrate is introduced for filtration through the inlet 21, for example, tangentially from the outside and passes, as indicated by the arrows, the pores between the individual filter discs 17. The filtrate is then removed from the interior 23 of the disc filter via the outlet 22. In the backwashing example, an air-liquid mixture is passed into the interior 23 and pressed against the direction of the arrow between the filter discs from the filter. At the same time, the pressing of the discs 17 relaxed by reducing the spring force. The filter pores are thereby increased and at the same time the individual disks are set in rotation by the backwashing. This ensures optimal cleaning of the filter surface.

The filter fineness is preferably about 50 μm. With a filter fineness of 100 μm, approximately 50% of the fibers are separated during the liquor filtration.

As explained in connection with FIGS. 4 to 6, a cross-flow filter 3 is used for fine filtration or microfiltration. For continuous operation with small separation limits, surface filtration with membranes as a filter layer is a sensible initial constellation. In the case of cross-flow filtration, the liquid to be filtered, in this case the coarse filtrate from the coarse filter 2a / b, flows in parallel along the filter membrane. The overpressure prevailing in the system ensures that a portion of the unfiltered material, in this case the coarse filtrate, passes through the membrane, transversely to the flow direction of the coarse filtrate. The entrained solids of the unfiltrate, d. H. of coarse filtrate on the membrane. With the parallel influxes of the membrane, the depositing solids are continuously entrained by the liquid and on the membrane, a balance between re-allocation and cleaning of the membrane is achieved. The depositing substances on the membrane, which are not entrained by the liquid flow, form the so-called gel layer.

A possible embodiment of such a cross-flow filter 3 is shown in FIGS. 4-6, wherein the filter here comprises a pressure housing 42 and at least one multitube membrane filter cartridge 40. Between the membrane filter cartridge 40 and the pressure housing 42, a filtrate 43 is formed. The multi-membrane membrane filter cartridge 40, as shown in more detail in Figures 5 and 6, a plurality of tubes 21 which extend in the longitudinal direction through the filter cartridge 40. The filter cartridge may be formed of ceramic material, wherein on the inside of the tube a little thick diaphragm layer may be arranged. The

Pore size is in a range of <= 2μm preferably <= 0.4μm, depending on the application. In the filtration occurs unfiltered, here coarse filter from the coarse filter 2 a / b in the tubes 21 of the filter cartridge 40, passes through the membrane in the tubes 21 and the ceramic of the filter candle and leaves the surface 41 of the filter cartridge 40 as a filtrate and enters the Filtratraum 43, where it can be withdrawn as a filtrate. The unfiltered material flowing through the tubes 21 leaves the cross-flow filter 3 and can be recirculated to the cross-flow filter are fed to maintain a Unfiltratstrom through the filter as will be explained in more detail below. Since the cleaning in breweries also hot cleaning liquids are used, the temperatures up to 90 ⁰ C, a cross-flow filter assembly of ceramic material is particularly suitable.

The device according to the invention and the method according to the invention can be used, for example, for cleaning fluids from CIP systems, e.g. for brewhouse cleaning or for cleaning in the bottle cellar.

The method according to the invention and the device according to the invention are explained in more detail below, in particular in connection with the bottle cleaning system shown in FIG.

FIG. 3 shows the main stages of a bottle cleaning machine with a bottle insert 53. After a residual emptying, the bottles pass successively through the pre-wetting 34 and the pre-wetting 35 and then pass through the pre-wetting bath. This is followed by the longest and most intensive treatment in the main spa 28, where most of the dirt and most of the contaminants dissolve. This also applies to the labels and the labeling glue. In a Nachlaugebad 37, d. H. In a first rinsing zone, the bottles are again cleaned internally and externally and can then be sprayed with hot water inside and outside with a spray device 38/39. Subsequently, there is still a treatment with cold and fresh water in a corresponding device 50. At the end of the bottles are delivered via a bottle delivery 54.

The inventive device for processing of cleaning liquid, here z. B. main liquor or supplement or a cleaning liquid of a CIP system is shown in Figure 1.

Hereinafter, the invention for cleaning liquor z. B. main liquor or lye described. However, the method or apparatus described in connection with Figure 1 is also applicable to another cleaning fluid, e.g. a brewery CIP plant, suitable.

The device according to the invention is connected via a line 24 to a reservoir for the cleaning liquor, for example, a main lavatory or a Nachlaugebad. Furthermore, the device comprises a pump 9 via which the cleaning solution into the Pumping device according to the invention can be pumped. In addition, the device 1 according to the invention here has two coarse filters 2a / b, which are arranged parallel to one another. The coarse filters 2a / b are for example disc filters as they were explained in more detail in connection with Figures 2a / b. The coarse filters 2a / b filter out particles of a size> 50 μm. Although not shown here, several coarse filters can be arranged parallel to each other and operated alternately for cleaning purposes. Although not shown, several coarse filters 2a could also be connected in series in series with several coarse filters 2b in series.

After coarse filtration, the coarse filtrate is passed to membrane filtration as shown by arrow G. Before the cross-flow filter 3, which has been explained, for example, as in connection with FIGS. 5-6, a pump 10 is arranged. The cross-flow filter 3 comprises a Filtratableitung 7, in turn, the valve 16 is arranged. The device further comprises a return line 4, through which the coarse filtrate is passed through the cross-flow filter 3 in the circle K. To adjust the flow, a control valve 15 is provided. Thus, the coarse filtrate moves on the membrane or membranes through the cross-flow filter 3, leaves the filter 3 and is circulated again via the pump 10 to the cross-flow filter 3, and indeed together with new coarse filtrate the coarse filters 2a / b. The device further comprises a feedback device 5 for backwashing the coarse filters 2a / b. As rinsing liquid, the coarse filtrate circulating in the circle K is advantageously used here. For this purpose, a discharge line 6 is provided, which is connected to the backwashing device 5. Thus, a predetermined portion of the recirculated unfiltered or coarse filtrate is passed into a washing container of the backwashing device 5. The backwash amounts are approximately at 0.1% - 0.5% of the throughput, z. B. at a filter amount in a size range of 1 - 10 m ³ lye per hour. By diverting the coarse filtrate from the cross-flow filter, a concentration of impurities is prevented, and this discharged coarse filtrate can be used in a skilful manner for backwashing. The backwashing device 5 further comprises a supply for scavenging air with a corresponding valve 25. The air coarse filtrate mixture can then be forced back into the coarse filter 2a / b via the pipe 26, after which it is conveyed with the dirt into the outflow 27. For this purpose, corresponding 3 / 2wegventile 13, 14, 11, 12 are provided, which can be switched so that in each case one filter is backwashed, while the other is in operation. Before and behind the filters 2a, b corresponding pressure sensors can be arranged, which determine the differential pressure in front of and behind the corresponding coarse filters 2a, b, which is compared with a desired value. If the measured differential pressure exceeds the predetermined desired value, then a backwashing process is initiated for a corresponding filter.

The derivative 6 branches off here from the annular guided return line 4. However, it would also be possible that this derivative 6 attaches directly to the output of the cross-flow filter. Advantageously, the discharge line 6 is arranged in a region from the rear end A of the cross-flow filter 3 to the point B at which new coarse filtrate is supplied from the filters 2a / b to the circuit K. The device may comprise a further branch line 8 for discarding a portion of the circulated coarse filtrate. If, for example, during the purification of the main liquor, the concentration in the circuit K is too high, a certain part can additionally be rejected via the discharge line 8. For this purpose, the valve 29 is provided. Before and after the cross-flow filter module, pressure sensors (not shown) may be arranged to measure the pressure difference, i. measure the transmembrane pressure. This differential pressure is compared with a setpoint. If the determined differential pressure exceeds the desired value, coarse filtrate, which is conducted in the circuit K, is diverted.

In the treatment of leach liquor can via the branch line 8, the circulated coarse filtrate also for pretreatment, d. H. For example, be directed to Vorlaugebad. Coarse filtration is sufficient for the quality of the cleaning solution in the pre-bath. Moreover, it is advantageous here that in the coarse filtrate, the surfactants were not filtered out and remain in the liquor. The branch line 8 starts here at the return line 4, but can also, as described above, adjoin the cross-flow filter.

The method according to the invention is first of all explained in more detail in connection with the cleaning of the main liquor of a main wash bath 28 of a bottle washing machine 10. First, via a pump 9 via the line 24 contaminated cleaning liquor is pumped from the Hauptlaugebad 28 in the device 1 according to the invention. Contaminated cleaning liquor passes through the coarse filter 2a / b, wherein the valves 11/12, 13/14 are connected so that the cleaning liquor flows through the filter in the direction of arrow to the line 30. The coarse filters 2a / b are decoupled from the purge line 26. The coarsely filtered cleaning liquor is then pumped via the pump 10 into the cross-flow filter 3. Transverse to the flow direction of the coarse filtrate, the coarse filtrate passes through the membrane and is thus finely filtered. The fine filtrate is returned to the main blast bath 28 via the line 7 when the valve 16 is open. leads. The coarse filtrate that passes through the cross-flow filter 3 is guided via the return line 3 in the circle K wherein at point B new coarse filtrate is fed to the circuit. To prevent the concentration of impurities in the circuit K, a certain part of the coarse filtrate via the line 6 of the backwashing 5, and a rinsing of the backwashing 5 is supplied. In this case, a certain part can be continuously removed from the circuit K or clocked at certain time intervals, a certain amount of coarse filtrate are derived. This discharged coarse filtrate, which then stores in the container of the backwash 5 can then be used in an advantageous manner to backwash one of the two coarse filter 2a / b.

For backwashing the coarse filter 2a / b, for example, the valve 13 is switched so that the backwash line 26 is connected to the coarse filter 2a, the coarse filter 2a, however, is not further connected to the line 30. Further, the valve 11 is adjusted so that the coarse filter 2a is connected to the drain 27, but not further with the line to the pump 9. For backwashing while air is injected into the washing. The air coarse filtrate mixture is then forced back through the pipe 26 through the filter 2a and then carried with the dirt into the drain. While the coarse filter 2a is backwashed, the valves 12/14 remain in a position in which the filter 2b takes over the coarse filtration, the cleaning liquor being conducted in the direction of the arrow into the conduit 30. After backwashing the valves 11/13 are returned to their working position, so that the coarse filtration can also be done again on the filter 2 a. Subsequently, the coarse filter 2b can then be backwashed in the same way by corresponding switching of the valves 11/12/13/14. As described above, the backwash operation for a coarse filter 2 can be initiated when the measured pressure difference before and after the coarse filter exceeds a certain setpoint. This ensures that the cleaning solution can be continuously processed and that the process does not have to be interrupted during backwashing. The fact that at the same time a concentration of the cleaning liquor in the cross-flow filter circuit K is prevented, the cross-flow filter does not increase, so that a continuous operation is possible. Should the concentration in the circuit K become too large, it is additionally possible to discharge coarse filtrate from the circuit K via the line 8 by opening the valve 29 accordingly. This discharged coarse filtrate is then discarded. Advantageously, the concentration can be prevented here without a large feed container is necessary. Thus, small volumes can be realized in the filtration unit, resulting in a minimized heat radiation. Furthermore, the whole system can be under pressure, resulting in minimized pumping power. In addition, small filling volumes offer the advantage of increasing the availability of the bottle washing machine, since it is not necessary to refill the bottle washing machine when starting up the filtration system.

In the purification of lye, the procedure is as explained in connection with the main liquor. Again, coarse filtrate from the membrane filtration circuit is used for backwashing, as previously discussed. In contrast to the previous embodiment, however, if necessary, coarse filtrate discharged via the line 8 and not discarded, but fed to a Vorlaugebad 32.

Figure 7 shows the basic scheme of a stack tank CIP system (Cleaning in Process). Such a plant 70 has a fresh water tank 71, a stack water tank 72, a disinfecting liquid tank 73, an acid tank 74 and a leach tank 75. Furthermore, a CIP unit can also have a feed for lye concentrate 76, for acid concentrate 77 and for disinfectant concentrate 78. The detergent concentrates 76, 77, 78 are diluted with the cleaning water in the corresponding disinfecting liquid, acid, or lye tanks 73, 74, 75 to the appropriate concentration. Via the line 79, the corresponding cleaning liquid from the tanks 73, 74, 75 are supplied to the object to be cleaned (tanks with cleaning device, piping, etc.) and are returned to the corresponding tanks via the return line 80. Via a line 24, not shown, the corresponding cleaning liquid from the tanks 73 or 74 or 75 of the device shown in Figure 1 can then be supplied. The fine filtrate can then be fed again to the respective tank 73, 74 or 75 via the fine filtrate line 7 shown in FIG. The coarse filtrate discharged via the outflow line 8 in FIG. 1 can be discarded.

It is advantageous that the same flow chart can be used for the main liquor and liquor purification of a bottle cleaning machine 10 as well as for CIP plants 70. This brings manufacturing advantages with it, since the same device can be built for all applications, which differs only by the pore size of the membrane of the cross-flow filter 3. Thus, the cleaning fluid can be replaced by a cheap device to be cleaned. Because the coarse filtrate discharged in the membrane filtration circuit is not completely discarded but used for backwashing, process media and energy can be saved.

The previous embodiments were described in particular in connection with cleaning fluids, which are incurred in particular in bottle washing machines and CIP systems in breweries. However, the method according to the invention and the device according to the invention can also be used for the treatment of cleaning liquids in other food-processing establishments (eg milk or juice). Also in Pharmabetrieben resulting cleaning fluids can be processed according to the present invention. Also in plastic recycling operations arise in particular in the cleaning of cleaning fluids, which can be prepared according to the present invention.

In plastics recycling, for example: In the first stage of wet scrubbing, the previously shredded bottles (flakes) are soaked in process water and fed to the hot lye scrub. There, the PET is washed hot with lye and surfactants and freed from adhering dirt, labels and glue residue. The wash liquor is treated according to the invention.

Then in a further stage, the PET can be rinsed several times hot. Demineralised fresh water is used in this process step and for the preparation of the wash liquor, otherwise treated process water is used. Also in this step, a preparation according to the invention is possible.

Claims

1. Device (1) for the treatment of cleaning fluids comprising:

at least one backwashable coarse filter (2a, b) for coarse filtration of the cleaning liquid,

a cross-flow filter (3) for fine filtration of the coarse filtrate from the at least one coarse filter (2a, b),

a return line (4), through which the coarse filtrate is passed through the cross-flow filter (3) in the circle (K),

a backwashing device (5) for backwashing the coarse filter (2a, b),

- A derivative (6), which branches off from the circle (K) and is connected to the backwashing (5), for backwashing the coarse filter (2a, b) with the through the cross-flow filter (3) circulated coarse filtrate ,

2. Apparatus according to claim 1, characterized in that at least two coarse filters (2 a, b) are arranged in parallel and are backwashed in alternation.

3. Apparatus according to claim 1 or 2, characterized in that the coarse filter (2a, b) filters out particles of a size> 50 microns.

4. The device according to at least one of claims 1 to 3, characterized in that the cross-flow filter (3) has a pore size in a range of <= 2μm, preferably <= 0.4 microns.

5. The device according to at least one of claims 1 to 4, characterized in that the device as a cleaning liquid main liquor from a Hauptlaugebad (28) of a bottle washing machine (10) processed and a Feinfiltratleitung (7) um- summarizes the Feiπfiltrat from the cross-flow filter (3) feeds the Hauptlaugebad again.

6. The device according to at least one of claims 1 to 4, characterized in that the device prepared as a cleaning liquid Nachlauge from a Nachlaugebad a bottle cleaning machine (10) and a Feinfiltratleitung (7), which again the fine filtrate from the cross-flow filter Nachlaugebad (37) supplies.

7. The device according to claim 5, characterized in that the circle (K) comprises a further branch line (8) for discarding a part of the circulated coarse filtrate.

8. The device according to claim 6, characterized in that the circle (K) comprises a further branch line (8) for supplying a part of the circulated coarse filtrate to a Vorlaugebad (32).

9. Device according to at least one of claims 1 to 4, characterized in that the coarse filter (2a, b) is disc filter.

10. The device according to at least one of claims 1 to 4, characterized in that the device prepares cleaning liquor or acid or disinfectant from a CIP system, and a fine filtrate comprises, the fine filtrate a corresponding alkali or acid or disinfectant liquid tank (75 , 74, 73).

11. A method for preparing cleaning fluids, wherein cleaning fluid is roughly filtered by means of a coarse filter (2a, b), the coarse filtrate to produce fine filtrate through a cross-flow filter (3) in the circle (K) through the cross-flow filter (3) is managed and a part of the coarse filtrate guided in the circle (K) is branched off and fed to a backwashing device (5), for backwashing the coarse filter (2a, b).

12. The method according to claim 11, characterized in that as a cleaning liquid main liquor from a Hauptlaugebad (28) of a bottle washing machine (10) is processed and the fine filtrate produced from the cross-flow filter (3) is supplied to the Hauptlaugebad again.

13. The method according to claim 11, characterized in that as a cleaning liquid Nachlauge from a Nachlaugebad (37) of a bottle washer system is treated and the fine filtrate from the cross-flow filter is again supplied to the Nachlaugebad.

14. The method according to claim 11, characterized in that cleaning solution or acid or disinfecting liquid is prepared from a CIP system as a cleaning liquid and the fine filtrate from the cross-flow filter is again supplied to a corresponding alkali or acid or disinfecting liquid tank.

15. The method according to claim 12 or 14, characterized in that the circulated coarse filtrate is further diverted a part which is discarded.

16. The method according to claim 13, characterized in that the circulated coarse filtrate is further branched off a part which is supplied to a pre-lye bath (32).

17. The method according to at least one of claims 11 to 16, characterized in that continuously a portion of the recirculated coarse filtrate is discharged.

18. The method according to any one of claims 11 to 16, characterized in that the discharged part of the coarse filtrate is removed in a clocked manner.

19. The method according to at least one of claims 11 to 17, characterized in that the cleaning liquid with the aid of at least two coarse filters arranged in parallel alternately or simultaneously filtered.

20. The method according to at least one of claims 11 to 19, characterized in that

Cleaning fluids, which are produced in breweries, in food processing plants, pharmaceutical companies or plastic recycling plants, are processed.